US5904850A - Settling device for a fluid containing liquid, gas and particulate material, as well as a cleaning device provided herewith and a method for cleaning waste water - Google Patents

Settling device for a fluid containing liquid, gas and particulate material, as well as a cleaning device provided herewith and a method for cleaning waste water Download PDF

Info

Publication number
US5904850A
US5904850A US08/913,888 US91388897A US5904850A US 5904850 A US5904850 A US 5904850A US 91388897 A US91388897 A US 91388897A US 5904850 A US5904850 A US 5904850A
Authority
US
United States
Prior art keywords
chamber
settling
caps
gas
oblique
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
US08/913,888
Other languages
English (en)
Inventor
Sjoerd Hubertus Jozef Vellinga
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Paques BV
Original Assignee
Paques BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Paques BV filed Critical Paques BV
Assigned to PAQUES B.V. reassignment PAQUES B.V. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: VELLINGA, SJOERD HUBERTUS JOZEF
Application granted granted Critical
Publication of US5904850A publication Critical patent/US5904850A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/28—Anaerobic digestion processes
    • C02F3/2866—Particular arrangements for anaerobic reactors
    • C02F3/2886—Two story combinations of the Imhoff tank type
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0042—Degasification of liquids modifying the liquid flow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B01D21/0045—Plurality of essentially parallel plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B01D21/0069—Making of contact surfaces, structural details, materials therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2433—Discharge mechanisms for floating particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2444—Discharge mechanisms for the classified liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2494—Feed or discharge mechanisms for settling tanks provided with means for the removal of gas, e.g. noxious gas, air
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/28—Anaerobic digestion processes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

Definitions

  • the present invention relates to a settling device for a fluid containing liquid, gas and particulate material, comprising:
  • a settling chamber which is to be filled with this fluid and in which there is fitted, for the trapping of gas bubbles, at least one cap having a ridge situated opposite a downwardly directed open side,
  • liquid-discharge means fitted close to the water level of the fluid
  • gas-discharge means for discharging from the settling chamber gas which has been trapped beneath the cap.
  • a settling device of this kind is known from EP-A1-0,244,029 and EP-A1-0,193,999. These publications describe caps which are fitted horizontally in overlapping connection and which are fitted to limit the top edge of a fermentation chamber so as to form a settling chamber above it. The caps trap gas bubbles rising from the fermentation chamber, whilst transfer of remaining fluid in the upward direction between the caps is permitted. The trapping of gas bubbles ensures that the fluid in the settling chamber is relatively still relative to the fluid in the fermentation chamber, the latter fluid being in a state of motion as a result of the rising gas bubbles.
  • the fact that the fluid present in the settling chamber is relatively still means that particles which are present therein and have been carried along from the fermentation chamber are able to settle, these particles being able to fall back between the caps to the fermentation chamber.
  • the settling devices known from these publications have the drawback, however, that, when major turbulences occur, bubbles can easily be passed between the caps and then make their way into the settling chamber, thereby having an adverse effect upon the settling in the settling chamber. Smaller gas bubbles, in particular will slip through easily between the caps.
  • the object of the present invention is, inter alia, to eliminate the above-mentioned drawbacks.
  • the primary object of the present invention is to provide a settling device in which a liquid, gas and particulate material can be separated, such that at the top of the settling device a liquid is collected which is largely free from particulate material and also, preferably, gas.
  • the at least one cap is disposed with its longitudinal axis at an angle to the water level, such that fluid supplied at the bottom of the settling chamber flows obliquely up, forced along the bottom of the at least one cap, whilst gas bubbles contained therein collect in the ridge of the at least one cap, and by the fact that the gas-discharge means trap below the water level the gas collected in the ridge of the at least one cap.
  • an obliquely placed cap should here be understood a body whose longitudinal axis, for the purpose of the oblique placement, runs at an angle to the water level (or horizontal) and whose bottom side, viewed in a direction perpendicular to the longitudinal axis, the so-called transverse direction, for the purpose of forming a cap, likewise runs at an angle to the water level (or horizontal).
  • the ridge of the cap is in this case situated on the high side of the bottom side angled obliquely in the transverse direction.
  • a further advantage of the settling device according to the invention is that underneath the obliquely placed cap a laminar flow can be realized, which promotes the deposition of particles contained in the fluid.
  • This laminar flow is particularly able to be realized by the fact that the gas bubbles which disrupt the laminar flow, such as described above, are separated from the fluid and are separately discharged.
  • oblique-plate settling devices are known from the prior art, in which use is made of a number of flat plates placed obliquely in overlapping connection. In such plates, the bottom side, viewed in a direction perpendicular to the longitudinal axis (i.e. in the direction of the transverse axis of the plate), runs parallel to the water level (or horizontal).
  • Such oblique-plate settling devices are suitable for the treatment of fluids containing liquid and particles. If these fluids contain gas bubbles, however, these gas bubbles will lend additional motion to the fluid flowing along the plates, thereby discouraging particles contained in these fluids from settling and disrupting any laminar flow.
  • the settling device comprises a row containing a multiplicity of caps which are disposed in oblique, overlapping and parallel arrangement.
  • the fluid will then be forced to flow upward via the interspaces formed between the adjacent, overlapping caps.
  • gas contained in the fluid will enter more rapidly into contact with a plate and will subsequently be collected in a ridge, so that the disruptive influence of these gas bubbles upon the deposition of particles will be quicker to decline.
  • the trapping and discharge of gas collected in the ridge(s) can be realized in a variety of ways.
  • use can be made, for example, of an inverted funnel-like element fitted in the ridge on the inner side of the cap.
  • the narrow outlet of the funnel can in this case be connected to a pipe extending, for example, obliquely upward along the ridge, in order to discharge the gas upward via a separate duct, thereby preventing fluid close to the water level from being disturbed.
  • the gas-discharge means can comprise a collecting pipe which extends essentially horizontally through the ridges and which on the inner side of the caps, close to the ridges, is provided with gas inlets having, for example, inverted funnel-like elements.
  • the gas-discharge means can comprise a collecting cap extending essentially horizontally through the ridges.
  • a collecting cap which can match the oblique caps in terms of shape, will generally have a smaller width than the obliquely fitted caps.
  • An advantage of a horizontally extending collecting pipe or collecting cap is, inter alia, that the collecting pipe or collecting cap can simultaneously serve for the suspension and mutual positioning of the oblique caps in the settling chamber.
  • a collecting cap which extends through the ridges it is also possible to collect and discharge floatable particles in a simple manner. By disposing the essentially horizontally extending collecting pipe or collecting cap at a slight angle of inclination relative to the water level or horizontal the discharge of gas collected therein and any floating particles is promoted.
  • the oblique caps of the settling device according to the invention will generally be fitted at an angle of 30° to 80° to the horizontal. Preferably, this angle will measure 55° to 65°. If the angle is too large, the gas bubbles contained in the fluid will be insufficiently trapped by the caps. If the angle is too small, an upward flow is excessively hindered. The value which is admissible for this angle will largely depend upon the process conditions and the composition of the fluid to be treated. An angle of about 55°to 65°, such as, for example, an angle of about 60°, has been shown to produce good results under diverse process conditions and with respect to diverse compositions of the fluid to be treated.
  • the caps are essentially V-shaped in cross-section, the angle between the legs of the V being able to measure about 100° to 130°, preferably about 110° to 120°.
  • Such V-shaped caps are simple to produce by two plates being fastened together or by a plate being folded at a suitable angle.
  • a laminar flow between the caps, in which particles present in the fluid can easily be settled, can be realized according to the invention where the caps are fitted at mutual horizontal intervals of about 2 to 8 cm, preferably about 6 cm.
  • the invention further relates to a purifier for, for example, the anaerobic purification of waste water, comprising:
  • a degassing chamber which is situated next to the settling device and which is divided by a partition into a first, relatively gas-rich compartment and a second, relatively gas-starved compartment, both compartments being interlinked at the top side of the partition and the degassing chamber being here provided with a gas discharge, the gas-rich, first compartment being linked to the fermentation chamber and the gas-starved, second compartment opening out into the bottom of the settling chamber of the settling device, and
  • separating means fitted between the fermentation chamber and the settling chamber of the settling device, which separating means trap gas bubbles rising in the fermentation chamber and discharge them to the first compartment of the gas-collecting chamber and conduct particles deposited in the settling chamber back to the fermentation chamber.
  • sludge which cleans waste water supplied in an anaerobic environment to the fermentation chamber. Rising gas bubbles are thereby produced, which set the fluid in the fermentation chamber into violent motion, whereupon sludge particles and other particles swirl through the fluid.
  • the gas bubbles are trapped by the separating means and led away to the first compartment of a degassing chamber linked to the fermentation chamber. The gas bubbles will rise up in this first compartment and, as a result of the high gas-bubble concentration, produce an upward flow of fluid in this first compartment.
  • gas is able to escape from the fluid and larger, floatable particles will continue to float out of the fluid.
  • the escaped gas and the floating particles can then be discharged, after which a fluid remains which is poorer in gas and particles.
  • This fluid which is poorer in gas and particles, is subsequently conducted onward via a second compartment so as to reach the bottom of the settling chamber of the settling device.
  • the fact that the fluid undergoes a downward motion as it is conducted through the second compartment means that a portion of the gas bubbles which are still being transported can flow back in the opposite direction so as to escape from the fluid at the top of the degassing chamber and be able to be discharged.
  • the fluid is subsequently conducted via the settling device already described above, whereupon gas which still remains is further able to escape and particles which are still present are able to be deposited from the fluid.
  • waste water such as waste water from breweries, for example, or sludge-containing waste water
  • Various sorts of bacteria and supports therefor can be added to the fermentation chamber, depending upon the sort of waste water.
  • Biomass and/or sludge can be situated in the fermentation chamber for the anaerobic or aerobic purification of the waste water.
  • the escaping gas will usually comprise O 2 , CO 2 , H 2 , either alone or in combination with each other or with other gases.
  • the separating means herein comprise essentially horizontally fitted gas caps, which are disposed side by side and so that they overlap somewhat with their bottom ends, such that there is a vertical gap between the bottom ends of the adjacent gas caps to enable the particles deposited in the settling chamber to be conducted back to the fermentation chamber.
  • gas caps For the gas caps, a large number of gas caps known from the prior art can be used. Reference should particularly be made to those gas caps fitted above a fermentation chamber which are known from European patent applications EP-A1-0,193,999 and EP-A1-0,244,029 of the applicant, which gas caps, by being referred to as part of the present application, are herein incorporated.
  • the invention further relates to a method for the anaerobic or aerobic purification of waste water using a device according to the invention.
  • FIG. 1 shows a diagrammatic view in perspective of a purifier according to the invention
  • FIG. 2 shows a diagrammatic, partially exploded side view of FIG. 1;
  • FIG. 3 shows a cross-section according to the lines III--III in FIG. 2;
  • FIG. 4 shows a detail of FIG. 1, in which, however, the caps 12 are fitted in a different, alternative manner, and
  • FIG. 5 shows a diagrammatic representation of the path covered by a rising gas bubble in the settling device.
  • the figures show a cleaning device 1 according to the invention, more particularly provided with a settling device 2 according to the invention.
  • the cleaning device comprises a reaction chamber, such as a fermentation chamber 3 above which there is fitted a settling device 2.
  • the fermentation chamber 3 and the settling device 2 are separated from each other by means of separating caps 4 (shown in purely diagrammatic representation), as known from EP-A1-0,244,029 and EP-A1-0,193,999 (herein incorporated by reference).
  • the cleaning device further comprises a degassing chamber 5 comprising a first compartment 6 and a second compartment 7, which compartments are separated from each other by an oblique partition 8. At the top side of this partition 8, the compartments 6 and 7 pass into each other.
  • a discharge (not represented) for floating particles At the top of the degassing chamber 5 there is provided a gas discharge 9 and a spray device 10 for spraying water with the aim of releasing gas bubbles attached to floating particles from said particles.
  • the settling device 2 comprises a multiplicity of V-shaped caps 12, which are placed obliquely at an angle of 60° to the water level 11 of the fluid.
  • Each cap 12 has a downwardly directed open side 13 and an opposing ridge 14.
  • the angle ⁇ between the legs of the V-shaped cap measures about 110°.
  • liquid discharge means At the top of the settling chamber of the settling device there are fitted, close to the water level 11 of the fluid, liquid discharge means in the form of overflow holes 15. These overflow holes 15 form a connection to a drain 16.
  • the horizontal interval Z between two adjacent oblique caps here measures about 6 cm.
  • the oblique caps 12 are positioned relative to each other by means of an essentially horizontally extending, V-shaped collecting cap 17 and are suspended by means of those caps 17 in the settling chamber of the settling device.
  • This collecting cap 17 extends through the ridges 14 of the row of successive, mutually partially overlapping caps 12.
  • passages 18 are formed in the ridges of the oblique caps 14 for the conduction of, in particular, gaseous fluid.
  • the collecting cap 17 is preferably inclined somewhat obliquely toward the degassing chamber 5 and opens out into the degassing chamber 5. Gases collected beneath the collecting cap 17 and floating particles are then discharged automatically, as it were, to the degassing chamber.
  • the separating means 4 comprise a whole cap 30 and two half caps 19 fitted next to the latter and in somewhat overlapping arrangement.
  • the bottom ends of the caps 30 and 19 are fitted so that they overlap in such a way that a vertical gap 20 is here formed, which is delimited by the bottom end of the cap 19 situated above and the top face of the cap 18 situated below. Via this gap 20, particles and fluid are able to flow back to the fermentation chamber 3 below it.
  • Waste water is supplied to the fermentation chamber via means (not shown), preferably continuously.
  • the waste water is cleaned by the bacteria and/or other means located in the fermentation chamber, thereby generating gas such as O 2 , CO 2 , H 2 .
  • This gas formation sets the fluid in the fermentation chamber into violent motion, as a result of which particles located in the fermentation chamber start to float around.
  • the rising gas bubbles are in large part trapped by the caps of the separating means 4. As illustrated by the arrows 21 and 22, this trapped gas is conducted to the first compartment 6 of the degassing chamber 5.
  • the gas will further rise, thereby producing an upward flow of fluid.
  • Fluid from the fermentation chamber 3 will consequently be guided upward, whereupon many particles contained in the fluid will be carried along.
  • the larger gas bubbles will leave the fluid at the top of the degassing chamber 5 and will be able to be discharged via a gas discharge 9.
  • Floatable particles which are carried along with the fluid out of the fermentation chamber 3 will end up floating on the water level 23 at the top of the degassing chamber. These floating particles can subsequently be discharged and gas bubbles attached thereto are able to be released by means of the spray device 10.
  • the fluid As a result of the gas which rises from the fermentation chamber and from the separating means 4, the fluid, as is indicated by the arrow 24, will be transported further obliquely downward via the second compartment 7 to the bottom of the settling device 2. As it flows downward through the second compartment, a portion of the gas still present in the fluid can rise as bubbles counter to the flow direction and collect at the top of the degassing chamber 5, so as then to be dischargeable via a gas discharge 9. As is represented by arrows 25, at the bottom of the settling device 2 a portion of the fluid will flow back via the gaps 20 to the fermentation chamber, particles deposited in the settling device 2 being able to be carried along. As is represented by arrows 26, another portion of the fluid will be forced to flow along the obliquely fitted caps 12, after which finally, at the top of the settling device, fluid is discharged from the purifier via the overflow holes 15.
  • the gas and the lighter particles will then rise further until being trapped by the gas-discharge means fitted below the water level 11, in this case in the form of an essentially horizontally fitted collecting cap 17.
  • the gas and the lighter particles collect in the collecting cap 17 and flow via the openings 18 along the bottom of the collecting cap 17 to the degassing chamber 5, where the gas can further be discharged via the gas discharge 9 and the lighter particles via the discharge for these (not shown).
  • the fluid above the collecting cap 17 is virtually totally rid of gas and lighter, floatable particles, thereby promoting the further settling of heavier particles still contained in the fluid.
  • the uppermost layer of the fluid in the settling device i.e. the fluid layer located close to the water level 11, will be very low in particles floating through it. This fluid, which is very low in particles, can further be discharged as purified fluid via the overflow holes 15 and the discharge ducts 16.
  • the settling device according to the invention can be used in a variety of ways. Use in connection with the purifier which is here outlined is very advantageous, but by no means the only usage option. It will additionally be clear that the direction in which the cap(s) 12 is (are) obliquely fitted may vary. That is to say, with reference to FIGS. 1 and 2, that the caps 12 can also incline obliquely to the right instead of obliquely to the left, as represented), or obliquely to the front or obliquely to the rear, whilst, here too, variants lying therebetween are conceivable.
  • FIG. 4 shows a design variant of the settling device according to the invention.
  • the difference with FIGS. 1-3 is essentially that the obliquely placed caps 12 of FIGS. 1-3 are rotated by 180° relative to their obliquely running longitudinal axes and, in FIG. 4, are indicated as caps 12.
  • the caps 112 lie with their longitudinal side edges in sealing arrangement against the side walls 120 of the settling chamber 2.
  • Each cap 112 comprises, as it were, two open downward-facing sides 113 and two ridges 114.
  • the ridges 114 are in this case situated along the side walls 120 of the settling chamber.
  • each (V-shaped) cap 112 thus forms, as it were, two caps.
  • FIG. 5 shows, with reference to a detail of FIG. 4, the course of a gas bubble in the settling device according to the invention.
  • zone 121 the gas bubble rises essentially vertically until the gas bubble comes into contact with the cap 112.
  • zone 122 the gas bubble is then conducted along the bottom of the cap 112 to the ridge 114. Having arrived in the ridge 114, the gas bubble is conducted along the bottom of the ridge 114 to the collecting cap 117 (zone 123) so as subsequently to be discharged via the collecting cap 117 (zone 124).
US08/913,888 1995-04-10 1996-04-10 Settling device for a fluid containing liquid, gas and particulate material, as well as a cleaning device provided herewith and a method for cleaning waste water Expired - Fee Related US5904850A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
NL1000100 1995-04-10
NL1000100A NL1000100C2 (nl) 1995-04-10 1995-04-10 Bezinkinrichting voor een vloeistof, gas, en deeltjesvormig materiaal bevatten fluïdum alsmede een hiervan voorziene reinigingsinrichting en werkwijze voor het reinigen van afvalwater.
PCT/NL1996/000156 WO1996032177A1 (en) 1995-04-10 1996-04-10 Settling device for a fluid containing liquid, gas and particulate material, as well as a cleaning device provided herewith and a method for cleaning waste water

Publications (1)

Publication Number Publication Date
US5904850A true US5904850A (en) 1999-05-18

Family

ID=19760860

Family Applications (1)

Application Number Title Priority Date Filing Date
US08/913,888 Expired - Fee Related US5904850A (en) 1995-04-10 1996-04-10 Settling device for a fluid containing liquid, gas and particulate material, as well as a cleaning device provided herewith and a method for cleaning waste water

Country Status (20)

Country Link
US (1) US5904850A (pl)
EP (1) EP0820335B1 (pl)
JP (1) JP3138478B2 (pl)
KR (1) KR100232762B1 (pl)
CN (1) CN1080581C (pl)
AT (1) ATE181850T1 (pl)
AU (1) AU686940B2 (pl)
BR (1) BR9604896A (pl)
CA (1) CA2217744C (pl)
CZ (1) CZ286946B6 (pl)
DE (1) DE69603173T2 (pl)
DK (1) DK0820335T3 (pl)
ES (1) ES2133950T3 (pl)
HK (1) HK1018023A1 (pl)
NL (1) NL1000100C2 (pl)
NO (1) NO316964B1 (pl)
PL (1) PL180591B1 (pl)
SI (1) SI9620049A (pl)
TR (1) TR199701135T1 (pl)
WO (1) WO1996032177A1 (pl)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6309553B1 (en) 1999-09-28 2001-10-30 Biothane Corporation Phase separator having multiple separation units, upflow reactor apparatus, and methods for phase separation
US20030046912A1 (en) * 2001-09-07 2003-03-13 Paques Water Systems B.V. Three-phase separator and installation for biological purification of effluent
US6783009B1 (en) * 2002-05-24 2004-08-31 Meurer Industries, Inc. Solely-bent baffle for liquid treatment basin
US6863816B2 (en) 2002-06-17 2005-03-08 Dharma Living Systems, Inc. Tidal vertical flow wastewater treatment system and method
US20050079712A1 (en) * 2000-02-16 2005-04-14 Ziptronix, Inc. Method for low temperature bonding and bonded structure
US6881338B2 (en) 2002-06-17 2005-04-19 Dharma Living Systems, Inc. Integrated tidal wastewater treatment system and method
US20050120758A1 (en) * 2002-05-08 2005-06-09 Thies Edward L. Remote sump with film heater and auto purge
US20050194310A1 (en) * 2004-03-03 2005-09-08 Kazuo Yamamoto Zero excess sludge membrane bioreactor
US20050218071A1 (en) * 2003-02-28 2005-10-06 Dharma Living Systems, Inc. Integrated tidal wastewater treatment system and method
US20050279703A1 (en) * 2004-06-17 2005-12-22 Dharma Living Systems, Inc. Nitrogen removal system and method for wastewater treatment lagoons
US20060226069A1 (en) * 2005-04-08 2006-10-12 Mijodrag Gordic Waste water treatment apparatus
WO2007058557A2 (en) 2005-11-18 2007-05-24 Universidade Do Minho Novel anaerobic reactor for the removal of long chain fatty acids from fat containing wastewater
US20080190844A1 (en) * 2007-02-13 2008-08-14 Richard Alan Haase Methods, processes and apparatus for biological purification of a gas, liquid or solid; and hydrocarbon fuel from said processes
NL2002494C2 (nl) * 2009-02-04 2010-08-05 Advanced Tail End Oil Company N V Inrichting voor het in fracties separeren van een stromend vloeistofmengsel, doorstroomtank en werkwijze ter vervaardiging van een platen-inrichting.
CN101397255B (zh) * 2007-09-30 2012-10-03 青岛银科恒远化工过程信息技术有限公司 甲苯二胺合成工艺中催化剂的连续分离循环方法及其设备
US20120325468A1 (en) * 2011-06-24 2012-12-27 Baker Hughes Incorporated Fluid migration shut-off
US11668037B2 (en) 2020-04-24 2023-06-06 Whirlpool Corporation Turbidity removal system for an appliance

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE1012053A3 (nl) * 1998-06-30 2000-04-04 Biotim Naamloze Vennootschap Inrichting voor het biologisch zuiveren van verontreinigd water.
EP1806323A1 (en) 2006-01-05 2007-07-11 Biothane Systems International B.V. Process and reactor for anaerobic waste water purification
EP1806324A1 (en) 2006-01-05 2007-07-11 Biothane Systems International B.V. Process and reactor for anaerobic waste water purification
DE102006015538A1 (de) * 2006-03-31 2007-10-11 H. C. Starck Gmbh & Co. Kg Vorrichtung und Verfahren zur Herstellung von Verbindungen durch Fällung
DE202008017818U1 (de) 2008-08-12 2010-07-01 Voith Patent Gmbh Dreiphasen-Kaskadentrennvorrichtung
EP2065344A1 (en) * 2008-09-23 2009-06-03 Paques Bio Systems B.V. Settling device, purifier containing the settling device and method for anaerobic or aerobic water purification
DE202009017869U1 (de) 2009-04-29 2010-09-23 Envirochemie Gmbh Vorrichtung zum Trennen von gasförmigen, flüssigen und festen Stoffen in einem Bioreaktor
EP2404879A1 (en) * 2010-07-08 2012-01-11 Paques IP. B.V. Purifier comprising a solids separation device, and method for wastewater purification
JP5600525B2 (ja) * 2010-08-31 2014-10-01 株式会社神鋼環境ソリューション 上向流式の反応槽、該反応槽を用いた水処理方法、該反応槽を備える水処理装置
AT511542B1 (de) 2011-05-16 2017-01-15 Lenzing Technik Gmbh Vorrichtung zur abtrennung von gasen aus einer suspension
CN106075964B (zh) * 2014-10-14 2018-01-02 杭州小橙工业设计有限公司 用于污水沉淀澄清处理的装置、环保装置
EP3348522A4 (en) * 2015-09-09 2019-07-31 Almeida Junior, Ronaldo Leite AEROBIC BIOLOGICAL PROCESS FOR ACTIVATED SLUDGE SLUDGE WITH SOLID HYDRODYNAMIC SEPARATION AND HYDRODYNAMIC SEPARATOR FOR OPERATION IN AN EFFLUENT TREATMENT STATION
WO2017221297A1 (ja) * 2016-06-20 2017-12-28 フタバ産業株式会社 排気管
CN108786193B (zh) * 2018-06-27 2021-09-24 李海强 分流式沉砂池
CN109536373A (zh) * 2018-11-27 2019-03-29 南京先进激光技术研究院 一种自动排气泡试剂反应管
CN109718577B (zh) * 2018-12-25 2021-02-05 浙江国涛滤料科技有限公司 高效导流过滤器
KR102209284B1 (ko) * 2019-05-17 2021-01-29 챔프다이아(주) 고내열강 부품 가공용 세라믹 접합 공구 및 이의 제조방법
KR102263932B1 (ko) 2019-05-17 2021-06-11 챔프다이아(주) 고내열강 부품 가공용 세라믹 접합 공구 제조방법
KR102263930B1 (ko) 2019-05-17 2021-06-11 챔프다이아(주) 고내열강 부품 가공용 세라믹 접합 공구 제조방법
KR102263931B1 (ko) 2019-05-17 2021-06-11 챔프다이아(주) 고내열강 부품 가공용 세라믹 접합 공구
US20220258183A1 (en) 2019-06-27 2022-08-18 Paques I.P. B.V. Spiral-shaped separation device for fluid purification device
CN110565476B (zh) * 2019-09-09 2021-02-09 北京世纪立成园林绿化工程有限公司 一种有助于改善居住区热岛效应的道路雨水收集系统
CN110585797B (zh) * 2019-09-20 2020-09-18 江苏京晶光电科技有限公司 一种蓝宝石切削液过滤冷却装置及其使用方法
CN113796347B (zh) * 2021-09-19 2023-08-15 湖南省稔泰农业科技有限公司 一种池塘底泥增氧防溢器
KR102618110B1 (ko) * 2021-12-17 2023-12-28 블루센 주식회사 미세 기포 제거 기능을 포함하는 정유량 조절 장치
CN116908172A (zh) * 2023-07-20 2023-10-20 湖南锦络电子股份有限公司 一种片式钽电容废水处理用排液检测装置

Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1445439A (en) * 1922-04-13 1923-02-13 Imhoff Karl Method of letting off sludge from sludge-digesting tanks
US2889929A (en) * 1954-09-03 1959-06-09 Dorr Oliver Inc Combined anaerobic treatment and clarification unit
US3488926A (en) * 1968-03-08 1970-01-13 Harrworth Inc Separator for removing gas bubbles from flowing liquids
DE1936350A1 (de) * 1968-07-19 1970-01-22 Paul Gagliardi Vorrichtung zum Trennen von Gasen und Fluessigkeiten,insbesondere zur Entgasung von Kohlenwasserstoffen
FR2118609A5 (pl) * 1970-12-15 1972-07-28 Aspanger Kaolin Steinwer
US3849311A (en) * 1970-07-13 1974-11-19 Int Pollution Control Systems Device for removing oil and the like from water contaminated by oil or the like
US4115279A (en) * 1974-03-26 1978-09-19 Simon-Hartley Limited Apparatus for separation of oil from oil and water mixtures
US4132651A (en) * 1976-02-19 1979-01-02 Dejong Leendert W C Separating device to separate two liquids of different specific gravity
GB2021549A (en) * 1978-05-23 1979-12-05 Centrale Suiker Mij Nv Apparatus for the anaerobic purification of waste water
US4202778A (en) * 1977-10-31 1980-05-13 Ballast-Nedam Groep N.V. Separating device
EP0015680A1 (en) * 1979-03-09 1980-09-17 Imperial Chemical Industries Plc Fermentation process and apparatus
GB1585141A (en) * 1978-01-27 1981-02-25 Paterson Candy Int Apparatus for separating a discontinuous phase from a continuous phase
EP0193999B1 (en) * 1985-03-06 1988-01-27 Paques B.V. Plant for the anaerobic purification of waste water
US4749480A (en) * 1984-11-20 1988-06-07 Sulzer Brothers Limited Reaction vessel
EP0244029B1 (en) * 1986-05-01 1989-10-18 Paques B.V. Equipment for the anaerobic purification of waste water
US5338445A (en) * 1992-01-24 1994-08-16 Passavant-Werke Ag Module for a reactor for anaerobic waste water treatment
US5670039A (en) * 1995-05-26 1997-09-23 Harris; Ronald B. Linear solids removal unit

Patent Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1445439A (en) * 1922-04-13 1923-02-13 Imhoff Karl Method of letting off sludge from sludge-digesting tanks
US2889929A (en) * 1954-09-03 1959-06-09 Dorr Oliver Inc Combined anaerobic treatment and clarification unit
US3488926A (en) * 1968-03-08 1970-01-13 Harrworth Inc Separator for removing gas bubbles from flowing liquids
DE1936350A1 (de) * 1968-07-19 1970-01-22 Paul Gagliardi Vorrichtung zum Trennen von Gasen und Fluessigkeiten,insbesondere zur Entgasung von Kohlenwasserstoffen
US3849311A (en) * 1970-07-13 1974-11-19 Int Pollution Control Systems Device for removing oil and the like from water contaminated by oil or the like
FR2118609A5 (pl) * 1970-12-15 1972-07-28 Aspanger Kaolin Steinwer
US4115279A (en) * 1974-03-26 1978-09-19 Simon-Hartley Limited Apparatus for separation of oil from oil and water mixtures
US4132651A (en) * 1976-02-19 1979-01-02 Dejong Leendert W C Separating device to separate two liquids of different specific gravity
US4202778A (en) * 1977-10-31 1980-05-13 Ballast-Nedam Groep N.V. Separating device
GB1585141A (en) * 1978-01-27 1981-02-25 Paterson Candy Int Apparatus for separating a discontinuous phase from a continuous phase
GB2021549A (en) * 1978-05-23 1979-12-05 Centrale Suiker Mij Nv Apparatus for the anaerobic purification of waste water
USRE32597E (en) * 1978-05-23 1988-02-09 Gist-Brocades N.V. Apparatus for the anaerobic purification of waste water
EP0015680A1 (en) * 1979-03-09 1980-09-17 Imperial Chemical Industries Plc Fermentation process and apparatus
US4749480A (en) * 1984-11-20 1988-06-07 Sulzer Brothers Limited Reaction vessel
EP0193999B1 (en) * 1985-03-06 1988-01-27 Paques B.V. Plant for the anaerobic purification of waste water
EP0244029B1 (en) * 1986-05-01 1989-10-18 Paques B.V. Equipment for the anaerobic purification of waste water
US5338445A (en) * 1992-01-24 1994-08-16 Passavant-Werke Ag Module for a reactor for anaerobic waste water treatment
US5670039A (en) * 1995-05-26 1997-09-23 Harris; Ronald B. Linear solids removal unit

Cited By (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6623640B2 (en) 1999-09-28 2003-09-23 Biothane Corporation Phase separator having multiple separation units, upflow reactor apparatus, and methods for phase separation
US6309553B1 (en) 1999-09-28 2001-10-30 Biothane Corporation Phase separator having multiple separation units, upflow reactor apparatus, and methods for phase separation
US20050079712A1 (en) * 2000-02-16 2005-04-14 Ziptronix, Inc. Method for low temperature bonding and bonded structure
US20030046912A1 (en) * 2001-09-07 2003-03-13 Paques Water Systems B.V. Three-phase separator and installation for biological purification of effluent
US6758886B2 (en) * 2001-09-07 2004-07-06 Paques Water Systems, B.V. Three-phase separator and installation for biological purification of effluent
US7406843B2 (en) * 2002-05-08 2008-08-05 Whirlpool Corporation Remote sump with film heater and auto purge
US20050120758A1 (en) * 2002-05-08 2005-06-09 Thies Edward L. Remote sump with film heater and auto purge
US6971398B1 (en) 2002-05-24 2005-12-06 Meurer Research, Inc. Hydrodynamic-force-responsive baffle for liquid treatment basin
US6783009B1 (en) * 2002-05-24 2004-08-31 Meurer Industries, Inc. Solely-bent baffle for liquid treatment basin
US7378021B2 (en) 2002-06-17 2008-05-27 Worrell Water Technologies, Llc Tidal vertical flow wastewater treatment system and method
US6863816B2 (en) 2002-06-17 2005-03-08 Dharma Living Systems, Inc. Tidal vertical flow wastewater treatment system and method
US6881338B2 (en) 2002-06-17 2005-04-19 Dharma Living Systems, Inc. Integrated tidal wastewater treatment system and method
US20060237363A1 (en) * 2002-06-17 2006-10-26 Dharma Living Systems, Inc. Tidal vertical flow wastewater treatment system and method
US7214317B2 (en) 2002-06-17 2007-05-08 Dharma Living Systems, Inc. Tidal vertical flow wastewater treatment system and method
US20070199893A1 (en) * 2002-06-17 2007-08-30 Worrell Water Technologies, Llc Tidal Vertical Flow Wastewater Treatment System and Method
US7029586B2 (en) 2003-02-28 2006-04-18 Dharma Living Systems, Inc. Integrated tidal wastewater treatment system and method
US20050218071A1 (en) * 2003-02-28 2005-10-06 Dharma Living Systems, Inc. Integrated tidal wastewater treatment system and method
US7311833B2 (en) * 2004-03-03 2007-12-25 Kazuo Yamamoto Zero excess sludge membrane bioreactor
US20050194310A1 (en) * 2004-03-03 2005-09-08 Kazuo Yamamoto Zero excess sludge membrane bioreactor
US7347940B2 (en) 2004-06-17 2008-03-25 Worrell Water Technologies, Llc Nitrogen removal system and method for wastewater treatment lagoons
US20050279703A1 (en) * 2004-06-17 2005-12-22 Dharma Living Systems, Inc. Nitrogen removal system and method for wastewater treatment lagoons
US20060226069A1 (en) * 2005-04-08 2006-10-12 Mijodrag Gordic Waste water treatment apparatus
WO2007058557A2 (en) 2005-11-18 2007-05-24 Universidade Do Minho Novel anaerobic reactor for the removal of long chain fatty acids from fat containing wastewater
US20080190844A1 (en) * 2007-02-13 2008-08-14 Richard Alan Haase Methods, processes and apparatus for biological purification of a gas, liquid or solid; and hydrocarbon fuel from said processes
CN101397255B (zh) * 2007-09-30 2012-10-03 青岛银科恒远化工过程信息技术有限公司 甲苯二胺合成工艺中催化剂的连续分离循环方法及其设备
NL2002494C2 (nl) * 2009-02-04 2010-08-05 Advanced Tail End Oil Company N V Inrichting voor het in fracties separeren van een stromend vloeistofmengsel, doorstroomtank en werkwijze ter vervaardiging van een platen-inrichting.
WO2010090520A1 (en) 2009-02-04 2010-08-12 Advanced Tail-End Oil Company N.V. Device for separating a flowing medium comprising mixture into fractions, throughflow tank and method for manufacturing a plate separator device
US9067153B2 (en) 2009-02-04 2015-06-30 Advanced Technologies & Innovations B. V. Device for separating a flowing medium comprising mixture into fractions, throughflow tank and method for manufacturing a plate separator device
US20120325468A1 (en) * 2011-06-24 2012-12-27 Baker Hughes Incorporated Fluid migration shut-off
US11668037B2 (en) 2020-04-24 2023-06-06 Whirlpool Corporation Turbidity removal system for an appliance

Also Published As

Publication number Publication date
CZ286946B6 (en) 2000-08-16
NO316964B1 (no) 2004-07-12
EP0820335A1 (en) 1998-01-28
KR19980703756A (ko) 1998-12-05
CN1181026A (zh) 1998-05-06
HK1018023A1 (en) 1999-12-10
BR9604896A (pt) 1998-07-14
ES2133950T3 (es) 1999-09-16
NO974576L (no) 1997-12-09
JP3138478B2 (ja) 2001-02-26
DE69603173D1 (de) 1999-08-12
PL322740A1 (en) 1998-02-16
SI9620049A (sl) 1998-02-28
PL180591B1 (pl) 2001-03-30
DE69603173T2 (de) 1999-12-16
CA2217744A1 (en) 1996-10-17
KR100232762B1 (ko) 1999-12-01
CA2217744C (en) 2000-08-29
CZ318297A3 (cs) 1999-02-17
NO974576D0 (no) 1997-10-03
DK0820335T3 (da) 2000-01-24
ATE181850T1 (de) 1999-07-15
WO1996032177A1 (en) 1996-10-17
NL1000100C2 (nl) 1996-10-11
JPH10511893A (ja) 1998-11-17
AU686940B2 (en) 1998-02-12
EP0820335B1 (en) 1999-07-07
CN1080581C (zh) 2002-03-13
TR199701135T1 (xx) 1998-02-21
AU5163796A (en) 1996-10-30

Similar Documents

Publication Publication Date Title
US5904850A (en) Settling device for a fluid containing liquid, gas and particulate material, as well as a cleaning device provided herewith and a method for cleaning waste water
US4333835A (en) Vertical tube liquid pollutant separators
US4056477A (en) Separating apparatus for clarifying liquid
US4422931A (en) Oil concentrator
CA1119323A (en) Apparatus for the anaerobic purification of waste water
US4624791A (en) Method for improving bubble surface area exposure
EP0888246B1 (en) Flotation apparatus and process
US5049266A (en) Device and method for microbiological water treatment
US6030529A (en) Biological reactor including settler assembly
US4303528A (en) Purification treatment of a liquid waste
US4564447A (en) Purification apparatus
JP4284051B2 (ja) 排水の生物学的浄化のための三相分離装置および設備
US4213865A (en) Apparatus for separating sludge, oil and the like from contaminated water
CA2592056A1 (en) Aeration system for liquid
RU1836301C (ru) Устройство дл очистки сточных вод
US7044308B2 (en) Apparatus for the removal of suspended solids and entrained oil from an aqueous solution
AU678020B2 (en) A clarifier for the separation of solids in waste water
US5658461A (en) Sedimentation apparatus
US6149827A (en) Device for separating particles from a particle containing liquid and a method for cleaning such a device
MXPA97007818A (en) Sealing device for a fluid containing liquid, gas, and a particulate material as well as a cleaning device provided with it, and a method for cleaning water residues
JP3169117B2 (ja) 生物学的廃水処理装置
IE47097B1 (en) Apparatus for separating a discontinuous phase from a continuous phase
CN218262140U (zh) 一种污泥筛选装置及系统
JPH1094794A (ja) 有機性排水の嫌気性処理装置
JP2956200B2 (ja) 嫌気性廃水処理装置

Legal Events

Date Code Title Description
AS Assignment

Owner name: PAQUES B.V., NETHERLANDS

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:VELLINGA, SJOERD HUBERTUS JOZEF;REEL/FRAME:008828/0433

Effective date: 19970919

FPAY Fee payment

Year of fee payment: 4

FPAY Fee payment

Year of fee payment: 8

REMI Maintenance fee reminder mailed
LAPS Lapse for failure to pay maintenance fees
STCH Information on status: patent discontinuation

Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362

FP Lapsed due to failure to pay maintenance fee

Effective date: 20110518